An improved model for membrane characterization in forward osmosis

被引:28
作者
Martin, Jeffrey T. [1 ]
Kolliopoulos, Georgios [1 ]
Papangelakis, Vladimiros G. [1 ]
机构
[1] Univ Toronto, Dept Chem Engn & Appl Chem, 200 Coll St, Toronto, ON M5S 3E5, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
Forward osmosis; Permeability; Membrane modeling; Desalination; PRESSURE-RETARDED OSMOSIS; INTERNAL CONCENTRATION POLARIZATION; WASTE-WATER; POWER-GENERATION; FLUX BEHAVIOR; SEAWATER DESALINATION; REVERSE-OSMOSIS; ENERGY; DRAW; TRANSPORT;
D O I
10.1016/j.memsci.2019.117668
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
As a promising technology for industrial water recovery, forward osmosis (FO) requires a rigorous and accurate transport model to determine its efficacy for water recovery from challenging effluents, yet current models neglect the non-ideality of concentrated draw solutions, and mass-transfer boundary layers within the process. This work builds upon recent FO transport models and presents an improved FO-based membrane characterization method that addresses the non-ideality of concentrated draw solutions, physical properties that are not based on the bulk draw solution, and all instances of concentration polarization. Using the FO-based characterization method of the present work, consistent water permeability and structural parameter values are obtained with R-2 > 0.985 for multiple inorganic draw solutions. When compared to additional experimental FO transport data, improvements of up to 107% were observed over the existing FO-based characterization method. Using the modeling approach developed in this work, the assessment for a potential FO application is refined by providing the means for accurate process modeling and membrane characterization.
引用
收藏
页数:11
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